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Sinochem Quanzhou HDPE HXM 50100

    • Product Name: Sinochem Quanzhou HDPE HXM 50100
    • Factroy Site: Yudu County, Ganzhou, Jiangxi, China
    • Price Inquiry: admin@ascent-chem.com
    • Manufacturer: Ascent Petrochem Holdings Co., Limited
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    Specifications
    HS Code 212824
    Environmental Stress Cracking Resistance H >1000
    Water Absorption <0.01
    Molecular Weight Distribution Broad

    As an accredited Sinochem Quanzhou HDPE HXM 50100 factory, we enforce strict quality protocols—every batch undergoes rigorous testing to ensure consistent efficacy and safety standards.

    Packing & Storage
    Packing Sinochem Quanzhou HDPE HXM 50100 comes in 25 kg net polyethylene-lined woven bags, stacked on pallets for transport.
    Container Loading (20′ FCL) 20′ FCL: 25 MT Sinochem Quanzhou HDPE HXM 50100 in 25 kg bags, 1,000 bags, floor-loaded without pallets.
    Shipping Sinochem Quanzhou HDPE HXM 50100 is typically shipped as a non-hazardous polymer in 25 kg PP woven bags or 1,000 kg jumbo bags, palletized and shrink-wrapped for FCL/LCL sea freight. Keep dry, away from direct sunlight and heat. Standard export packaging from Quanzhou, China.
    Storage Store Sinochem Quanzhou HDPE HXM 50100 in a cool, dry, well-ventilated warehouse away from direct sunlight, heat, sparks, and open flames. Keep original bags or containers tightly closed to prevent moisture, dust, and contamination. Avoid contact with strong oxidizers. Use first-in, first-out stock rotation. Handle pallets carefully and avoid excessive stacking to prevent bag deformation or rupture. Ensure ventilation and grounding.
    Shelf Life Shelf life for Sinochem Quanzhou HDPE HXM 50100 is typically two years when stored unopened, dry, cool, ventilated, away from sunlight.
    Application of Sinochem Quanzhou HDPE HXM 50100

    Potable water distribution represents the largest verified downstream segment for Sinochem Quanzhou HDPE HXM 50100. The resin is specified as a bimodal high-density polyethylene pipe material and is converted into solid-wall pressure pipe classified as PE100 under ISO 12162:2009, carrying an MRS of 10.0 MPa and a design stress of 8.00 MPa at 20 °C with a design coefficient C=1.25. Compliance for potable water systems requires conformity to ISO 4427-1:2019 and ISO 4427-2:2019 for polyethylene pressurized water pipe, EN 12201-1:2011 and EN 12201-2:2011 for European projects, GB/T 13663.1-2018 and GB/T 13663.2-2018 for Chinese water supply networks, and NSF/ANSI/CAN 61 for North American potable water contact. Long-term hydrostatic strength is demonstrated through ISO 9080:2012 extrapolation to 50 years at 20 °C, and batch release testing follows ISO 1167-1:2006 at 20 °C and 80 °C. On production-scale pipe lines, the formulation is set at 100 parts by weight of virgin HXM 50100; black pipe incorporates 2.0–2.5 wt% carbon black masterbatch for UV stabilization and weathering resistance during outdoor storage, while non-black potable water grades use 2–4 wt% blue pigment masterbatch. In-house regrind from clean start-up scrap and sprues is limited to 10 wt% or less because higher rework fractions reduce slow crack growth margins; external post-consumer recyclate is not permitted under ISO 4427-1:2019 for pressure service. Downstream pipe extrusion is carried out on grooved-feed single-screw extruders with barrier screws and L/D ratios of 30:1–36:1; barrel zone settings range from 180 °C to 210 °C, adapter and die head temperatures are held at 200 °C to 220 °C, and melt temperature is controlled between 190 °C and 220 °C. Sustained melt temperatures above 230 °C accelerate thermal-oxidative chain scission and shorten notched pipe test lifetimes under ISO 13479, while on-line ultrasonic wall-thickness gauges are used to maintain dimensional stability during vacuum calibration and spray cooling. Finished product types include DN 20–1200 mm water mains, branch service laterals, distribution pipes, and relining pipes in SDR 26 through SDR 7.4, spanning PN 6.3 through PN 25 classes.

    ServiceSystem standardsMaterial and jointing test standards
    PE100 material classificationISO 12162:2009, ISO 9080:2012, ISO 1167-1:2006ISO 13479, ISO 13477, ISO 13478
    Pressurized potable water pipeISO 4427-1:2019, ISO 4427-2:2019, EN 12201-1:2011, EN 12201-2:2011, GB/T 13663.1-2018, GB/T 13663.2-2018NSF/ANSI/CAN 61, ISO 1167-1:2006
    Natural gas distribution pipeISO 4437-1:2014, ISO 4437-2:2014, EN 1555-1:2010, EN 1555-2:2010, GB/T 15558.1-2015, GB/T 15558.2-2015, ASTM D2513-20ISO 13477, ISO 13478, ISO 13479
    Butt fusion and electrofusionISO 21307:2017, ISO 12176-2:2011ISO 13953

    What governs slow crack growth resistance in natural gas distribution pipe made from HXM 50100?

    Slow crack growth resistance, rather than short-term burst pressure, governs the 50-year design life of natural gas distribution pipe extruded from HXM 50100. The material is supplied as PE100 under ISO 12162:2009, and pipe systems are manufactured to ISO 4437-1:2014 and ISO 4437-2:2014 for gas supply, EN 1555-1:2010 and EN 1555-2:2010 for European gas networks, GB/T 15558.1-2015 and GB/T 15558.2-2015 for Chinese gas distribution, and ASTM D2513-20 for North American thermoplastic gas pipe. The formulation on the extrusion line contains 100 parts by weight of virgin HXM 50100, 2.0–2.5 wt% carbon black masterbatch for black pipe or 2–4 wt% yellow pigment masterbatch for high-visibility gas lines, and clean in-house regrind limited to 10 wt%; external recyclate is prohibited because PE100 gas pipe must retain resistance to rapid crack propagation and slow crack growth. Downstream conversion uses grooved-feed single-screw extruders with L/D ratios of 30:1–36:1, barrel temperatures between 180 °C and 210 °C, and melt temperatures of 190 °C to 215 °C, after which the pipe is vacuum-calibrated, ultrasonically scanned for wall thickness and ovality, and cut into straight lengths or coils. On production-scale lines, black specks, die drool, and wall-thickness variation exceeding ±1% are frequently traced to incomplete masterbatch transition or worn screw mixing sections; these defects create local stress concentrations during slow crack growth. Jointing in the field follows ISO 21307:2017 butt fusion procedures for butt welding and ISO 12176-2:2011 for electrofusion couplers, with pipe ends scraped to remove the oxidized surface layer before facing. Qualification for slow crack growth resistance commonly includes notched pipe testing under ISO 13479, rapid crack propagation testing under ISO 13477, and full-scale critical pressure verification under ISO 13478 where project specifications require a critical pressure above 1.5 × MOP. Finished terminal products include black and yellow PE100 gas mains, service laterals, and distribution branches in DN 20–400 mm sizes, with SDR 17.6 and SDR 11 wall-thickness ratios commonly selected according to operating pressure and location class.

    In run-of-mine tailings, dredge discharge, and hydrotransport of mineral slurries, HXM 50100 is converted into thick-wall solid-wall pipe where service life is controlled primarily by abrasive wear and particle impingement rather than static pressure creep. There is no dedicated ISO slurry-pipe product standard; project specifications normally reference ISO 12162:2009 for PE100 material classification, ISO 9080:2012 for hydrostatic design basis, ISO 4427-2:2019 for pressure pipe dimensions, and ISO 21307:2017 for butt fusion. Published tabulated wear coefficients for HXM 50100 in high-solids slurry service are limited, so qualification is typically conducted by site-specific slurry loop or rotating-drum abrasion comparisons rather than by a single material constant. The extrusion formulation contains 100 parts by weight of virgin HXM 50100 and 2.0–2.5 wt% carbon black masterbatch; no mineral filler or abrasion filler is required because stiffening additives reduce slow crack growth resistance, and in-house regrind is limited to 10 wt% or eliminated for high-wear sections to avoid local property gradients. Downstream pipe production uses grooved-feed single-screw extruders with L/D ratios of 33:1 or higher, melt temperatures maintained between 190 °C and 215 °C, and controlled multi-stage cooling through vacuum calibration and water spray baths to reduce residual thermal stress in thick walls. Slurry flow velocity should be kept between 1.5 m/s and 6 m/s depending on particle size, solids specific gravity, and slope; below 1.5 m/s bed deposition risk rises, and above 6 m/s localized wear intensity increases with approximately the cube of velocity, with elbows and directional changes typically determining replacement intervals. Finished terminal products include tailings mains, dredge sleeves, hydrocyclone feed and underflow lines, flotation transfer pipes, mine dewatering risers, and process water return lines in pressure classes from PN 6.3 through PN 25.

    SDRNominal pressure at 20 °CDN 110 wall thicknessTypical slurry service
    SDR 26PN 6.34.2 mmLow-pressure transfer, overflow lines
    SDR 17PN 106.6 mmDredge discharge with booster stations
    SDR 13.6PN 12.58.1 mmTailings hydrotransport
    SDR 11PN 1610.0 mmMine dewatering, high static head
    SDR 7.4PN 2514.9 mmHigh-pressure hydrocyclone feed and shut-in pressure zones

    When HXM 50100 is specified for ground-source heat pump loop circuits

    When HXM 50100 is specified for ground-source heat pump loop circuits, the resin is typically extruded into 20–63 mm outside diameter SDR 9 and SDR 11 pipe coils under ASTM D3035 dimensional requirements and, where North American specifications apply, a PE4710 cell classification under ASTM D3350-21; the compounding ratio is 100 parts by weight of virgin HXM 50100 with 2.0–2.5 wt% carbon black masterbatch only where UV resistance is required for above-ground headers or exposed loops, and in-house regrind is limited to 10 wt%; the downstream process involves grooved-feed pipe extrusion at melt temperatures of 190–215 °C, vacuum calibration, coiling into 150–300 m lengths, and U-bend fabrication by butt fusion to ISO 21307:2017 or electrofusion to ISO 12176-2:2011, followed by pre-backfill pressure testing at 2.0 × the maximum operating pressure; terminal product types include vertical U-bends, horizontal slinky loops, pond/lake loops, and header manifolds for closed-loop ground-source heat pump systems.

    Qualifying industrial effluent pressure pipe through chemical resistance data and joint integrity

    Industrial effluent pressure pipe produced from HXM 50100 carries corrosive aqueous streams in chemical parks, electroplating facilities, and waste treatment plants, and is qualified through ISO 4427-1:2019 and ASTM F714-19 for pressure pipe dimensions plus chemical resistance classification under ISO/TR 10358 and immersion testing under ISO 4433-1:1997 for site-specific process liquors; the formulation uses 100 parts by weight of virgin resin, 2.0–2.5 wt% carbon black masterbatch for black pipe or 2–4 wt% identification masterbatch for striped process lines, and in-house regrind is limited to 10 wt% or eliminated in strongly oxidizing media because regrind thermal history shifts oxidation induction time; the conversion route uses grooved-feed pipe extrusion at melt temperatures of 190–215 °C, ultrasonic wall-thickness monitoring, vacuum calibration, and butt fusion to ISO 21307:2017; terminal product types include acid/alkali transfer lines, industrial drainage mains, leachate collection pipes, scrubber water discharge lines, and double-containment HDPE pipes for secondary containment duty. HDPE should not be specified for concentrated nitric acid, oleum, or chlorinated solvents above 40 °C without immersion testing, because oxidative attack can reduce elongation at break below acceptance thresholds.

    For submerged marine intake and outfall service, HXM 50100 is butt-welded into continuous strings for desalination plant intakes, power plant cooling water lines, and sewage outfalls, where the design basis demands 50-year slow crack growth retention under tidal current and seabed settlement loads. Pipe systems are specified to ISO 4427-1:2019, ISO 4427-2:2019, and EN 12201-2:2011, with field welding qualified under ISO 21307:2017 and post-weld hydrostatic testing under ISO 1167-1:2006 or project hydrotest procedure. The extrusion formulation consists of 100 parts by weight of virgin HXM 50100, 2.0–2.5 wt% carbon black masterbatch for UV stabilization during above-ground onshore staging, and in-house regrind capped at 10 wt%; external recyclate is not used in submerged pressure-rated pipe. The downstream marine fabrication process involves shore-side butt welding of 12 m or 18 m pipe lengths into strings of 100–500 m, placement of concrete ballast weights, float-and-sink installation, and submerged alignment; long runs are filled with water to control buoyancy and reduce lateral deflection from tidal currents. Finished terminal product types include desalination intake and brine outfall lines, power plant once-through cooling water intakes, sewage outfalls, and subsea HDPE pipelines installed by controlled submergence.

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    Certification & Compliance
    More Introduction

    Sinochem Quanzhou HDPE HXM 50100 is a bimodal high-density polyethylene resin produced on a hexene-1 comonomer platform. The model designation identifies it within the Sinochem Quanzhou polyolefin portfolio as a pressure-pipe and thick-wall industrial extrusion grade, not a general-purpose film or blow-moulding resin. Its specification envelope is anchored by two routine indices: density at 0.950 g/cm³ when measured to ISO 1183-1 or ASTM D1505, and melt mass-flow rate at 190 °C under 2.16 kg in the class range 0.08–0.12 g/10 min when measured to ISO 1133-1:2022. The high-load melt index at 190 °C/21.6 kg is a stronger production-control variable because it reflects the high-molecular-weight tail that governs slow-crack-growth resistance.

    Because grade-specific lot data are controlled by the Sinochem Quanzhou certificate of analysis, the values in Table 1 should be read as a reported class envelope rather than guaranteed lot minima.

    Table 1. Reported class envelope for Sinochem Quanzhou HDPE HXM 50100.

    PropertyMethodReported class value
    DensityISO 1183-1 / ASTM D15050.948–0.952 g/cm³
    Melt mass-flow rateISO 1133-1:2022 / ASTM D1238, 190 °C/2.16 kg0.08–0.12 g/10 min
    High-load melt indexISO 1133-1:2022 / ASTM D1238, 190 °C/21.6 kg6.0–8.0 g/10 min
    Flow rate ratioCalculated from 21.6 kg/2.16 kg60–80
    Tensile yield stressISO 527-2 / ASTM D638-1421–25 MPa
    Elongation at yieldISO 527-28–10 %
    Elongation at breakISO 527-2>600 %
    Flexural modulusISO 178900–1100 MPa
    Environmental stress-crack resistance, F50ASTM D1693, Condition B, 100 % Igepal>1000 h
    Pennsylvania notch testASTM F1473, 80 °C, 2.4 MPa>1000 h
    Notched Charpy impact, 23 °CISO 179-1/1eANo break
    Vicat softening temperature, A50ISO 306121–124 °C
    Minimum required strength, 20 °C, 50 yearsISO 9080 / ISO 1216210 MPa MRS, PE100 class
    Oxidative induction time, 200 °CISO 11357-6>20 min

    What Makes the Bimodal Architecture of HXM 50100 Different from Unimodal Pipe Resins?

    The long-term failure mode of interest in pressure pipe is slow crack growth through the amorphous tie-molecule network. A bimodal molecular weight distribution gives HXM 50100 a low-molecular-weight fraction that lowers melt viscosity and a high-molecular-weight fraction that increases the number of tie molecules between adjacent crystalline lamellae. Unimodal high-density polyethylene with the same 0.950 g/cm³ density and similar low-load melt index may show significantly shorter failure times under stress because fewer long chains survive crystallisation to form load-bearing connections. The difference is not captured by density or melt index alone; it is measured with ASTM F1473 PENT and ASTM D1693 ESCR. Under PENT conditions of 80 °C and 2.4 MPa, PE100/PE4710 class resins such as HXM 50100 are typically specified to exceed 1000 h; general-purpose unimodal HDPE of similar density may fall below 100 h under identical stress.

    Hexene-1 comonomer placement produces short-chain branches in the polymer backbone, but the complete chain architecture is not publicly disclosed. The practical consequence is stronger weld performance and higher creep-rupture strength. Under ISO 9080, the resin is associated with an MRS of 10 MPa at 20 °C for 50 years, placing it in the PE100 class under ISO 12162. A general-purpose injection-moulding or blow-moulding grade of the same density would not carry this classification. Published data for the specific branch distribution and molecular weight moments of Sinochem Quanzhou HXM 50100 are limited; the classification is established by pipe-level hydrostatic testing rather than resin-level melt index alone.

    Capillary rheometry at 190 °C with Bagley correction shows pronounced shear thinning in this resin class. The viscosity at 100 s⁻¹ is typically above 5000 Pa·s, while at 1000 s⁻¹ it may fall below 1000 Pa·s. This non-Newtonian response allows high-speed pipe extrusion despite the low low-shear melt index. The melt strength is high enough for large-diameter thick-wall pipe but is not optimised for blown-film bubble stability or parison sag in extrusion blow moulding. These processing differences are measured by the flow rate ratio and extensional viscosity behaviour, not by the low-load melt index alone.

    During pipe extrusion on a 90 mm single-screw extruder with a L/D 30:1 barrier screw and a grooved feed section, the feed throat is kept at 40–70 °C, barrel zones are ramped from 180 °C to 220 °C, and adapter and die zones are held at 215–230 °C to maintain melt temperature below 240 °C. Screw speeds above 80 min⁻¹ may generate excessive shear heating; the resulting melt-temperature overshoot can degrade the high-molecular-weight tail and reduce PENT while also producing unmelted material in thick-wall pipe. Melt pressure at the breaker plate typically falls between 200 bar and 350 bar depending on pipe diameter, screw speed, and haul-off rate. Pressure fluctuations above 15 bar at constant speed indicate feed instabilities.

    Pre-drying is not normally required below 60 % RH, but desiccant drying at 70–80 °C for 4 h is applied to cold or wet bags because surface condensation can create pinholes and internal voids during pipe extrusion. After running HXM 50100, purging with a high-viscosity HDPE purge material is recommended because the high-molecular-weight fraction can remain in dead zones and later contaminate low-viscosity grades. Purging temperature should be raised to 220–230 °C and screw speed reduced to 10–20 min⁻¹ until the melt flow is homogeneous.

    Comparative Performance Against PE80 and General-Purpose HDPE Grades

    Substituting HXM 50100 for a PE80 resin changes the design stress calculation. PE80 resins are assigned an MRS of 8 MPa at 20 °C under ISO 9080; PE100 resins are assigned 10 MPa. With a service coefficient of 1.25, the design stress becomes 8.0 MPa for HXM 50100 and 6.3 MPa for PE80. Accordingly, SDR 11 PE100 pipe is commonly rated at 16 bar for water at 20 °C, while PE80 SDR 11 is rated at 12.8 bar under the same calculation. The practical result is that a PE100 pipe can carry a higher operating pressure at the same SDR or allow a thinner wall at the same pressure.

    Compared with general-purpose blow-moulding HDPE of similar density, HXM 50100 has a lower melt index and broader molecular weight distribution. This improves ESCR and creep-rupture strength but creates excessive parison sag for extrusion blow moulding. The material is therefore not interchangeable with blow-moulding grades in the same plant portfolio without re-engineering the die gap, parison programming, and cooling time.

    Table 2. Compliance checks by application for Sinochem Quanzhou HDPE HXM 50100.

    ApplicationGoverning standardsCritical propertyRequirement
    Potable water pressure pipeISO 4427, EN 12201, NSF/ANSI 61Organoleptic migration, chlorine resistancePipe-level certification required; resin-only data not sufficient
    Natural gas distributionISO 4437, ASTM D2513Rapid crack propagation, weld integrity, slow crack growthPipe-level testing under ISO 13477 or ASTM F3183
    Mining slurry and industrial effluentISO/TR 10358Chemical compatibility, abrasionFluid-specific immersion data required
    Above-ground UV serviceISO 16871Weathering resistanceCompound with 2.0–2.5 wt% carbon black masterbatch

    When HXM 50100 Is Used in Aggressive Media and Above-Ground Installations

    Chemical compatibility with chlorinated water, organic solvents, or mixed industrial effluents must be established through ISO/TR 10358 tabulations and immersion testing on pipe, not inferred from ESCR alone. Resistance of HDPE to chlorine-induced stress cracking is influenced by molecular weight, branch content, and stabiliser formulation. The natural resin without a chlorine-resistant formulation may not satisfy all potable-water utilities. Published data for HXM 50100 in hot chlorinated water service are limited. Utilities requiring long-term chlorine resistance should specify pipe-level testing under the applicable national water-contact standard and avoid reliance on resin data alone.

    For above-ground or outdoor storage, the natural pellets must be compounded with 2.0–2.5 wt% carbon black masterbatch to meet the weathering criteria of ISO 16871. Without this addition, ultraviolet exposure may cause surface embrittlement and loss of tensile impact strength. Continuous service above 20 °C requires pressure derating in accordance with ISO 13760 or the manufacturer’s pressure-temperature table. Continuous exposure above 60 °C shifts the failure mechanism toward oxidative degradation; in this regime, hydrostatic lifetime is no longer predicted by room-temperature creep-rupture data alone.

    Pipe extrusion from HXM 50100 is applied to buried potable water mains, gas distribution laterals, mining slurry and tailings lines, agricultural irrigation, and industrial effluent systems. The controlling acceptance criteria in these uses are butt-fusion weld strength per ISO 21307 or ASTM F2620, resistance to rapid crack propagation per ISO 13477 where required, and slow-crack-growth performance at the weld bead or external scratch. Thick-wall pipe processed from this resin requires controlled internal cooling; residual stresses introduced by uneven die-to-haul-off temperature gradients reduce crack growth resistance. Procurement should confirm actual lot values for density, MFR, flow rate ratio, tensile yield, ESCR, and PENT against the Sinochem Quanzhou certificate of analysis rather than substituting nominal class values for certification testing.

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